Method for injection stretch blow molding

ABSTRACT

As the hot parison method stretch blow molding, the temperature distribution of the inner side of the body wall of the injection molded preform is changed to the gentle gradient slope shape temperature distribution from the mountain shape not by the external application of heating but by the preform itself so that the bottle which the top load value is improved can be prepared. The preform which is injection molded is mold-released in a high temperature state. The inner side cooling of the preform after mold-release is continued by the injection core. The inner side cooling is terminated by mold-release of the preform from the injection core. The preform is left in a hollow state. The leaving time is made as the temperature-averaging time of the preform. The preform is maintained until the outer surface temperature drops to the stretch blow molding temperature thereafter the peak temperature. In the molding temperature region, the stretch blow molding of the thin-wall hollow molded article is conducted.

BACKGROUND OF THE INVENTION

1. Field of the Invention

The present invention relates to a method that an injection molded preform is transferred to a blow mold and is stretch blow molded to a thin-wall hollow molded article such as a bottle or a wide-mouth container and the like.

2. Description of the Related Art

The injection stretch blow molding is known that material resins such as polyethylene terephthalate(PET), polypropylene(PP), polycarbonate(PC), polyethylene (PE) and the like are carried out to melt by an injection apparatus and inject and fill into a cavity of an injection mold, and a closed-end preform which a body part and a neck part are integrally molded by the injection mold is transferred to a blow mold by releasing from the mold while at a high temperature state, and in the blow mold, by means of elongation of a stretch rod and air blow the perform is formed to a packaging container such as a bottle having a thin-wall body part or a wide-mouth container and the like.

As the injection stretch blow molding methods, the method which a preform is released from the injection cavity mold and an injection core, and is transferred to the blow mold while a neck part of the preform is supported by a neck mold (U.S. Pat. No. 5,364,585), and for an object to shorten the injection molding time, the method which the preform is released from the injection cavity mold while being supported by the injection core and the neck mold and a cooling of the preform is continued simultaneously to be transferring to the blow mold side (U.S. Pat. No. 5,589,130), have been disclosed.

The above mentioned conventional method which an injection molded preform is stretch blow molded immediately while in a high temperature state is called as a hot parison method or one-stage method, as contrasted with a cold parison method which an injection molded solid preform is heated to the mold temperature at the stretch blow molding. In case of the cold parison method, since a body part and a bottom part except a neck part are applied by heating from the external heating, the difference of high and low temperatures in the wall part during the stretch blow molding is small and a large difference is not made to the degree of the molecular orientation generated by the stretch so that a bottle having a high top load value can be obtained.

In case of the hot parison method, since the preform is in the high temperature state just as-injection molded, the temperature distribution in a cross section of the body wall is provided as a mountain shape which the temperature of the central part is high compared with the cooled inner and outer sides, and the temperature difference is big. The temperature difference gets small by the chance of the stretch blow molding, but is not eliminated completely, and the temperature difference provides the influence to compression strength as a result of the difference of degree of orientation of molecular orientation by stretch so that the top load value is considered incapable to provide as much as the value by the cold parison method.

As a means to shorten the cooling time after injection, in case of the conventional method which the preform is released from the injection cavity mold together with the injection core and a core cooling is continued even after the mold-release, by the inner side cooling by the injection core the temperature difference occurs in inner and outer sides so that the temperature distribution changes from a mountain shape to a slope shape of the temperature gradient having low inner side temperature. But along with the cooling time, the temperature difference between the inner and outer sides grows big and the temperature gradient is steep, and also since the inner side skin layer is formed thick, the stretch blow molding in the steep gradient temperature distribution is difficult so that the bottle with a good molding state can not be obtained.

In the temperature distribution of the slope shape which the temperature is provided lower toward the inner side of the body wall, since there is no protruding high temperature as the mountain shape, a formation of multiple layers generated from the difference of degree of orientation caused by stretch is difficult to generate. Accordingly, the inner and outer sides temperatures are made so as to get near by some measures to make the temperature distribution in gentle gradient, then the stretch blow molding is capable in the temperature distribution similar to the cold parison method, so that considering the hot parison method, the bottle having the high top load value can be molded.

As for polyethylene terephthalate of material resin, more improvement is provided than before and the material, which the whitening phenomenon of the preform does not generate even if the outer surface temperature is 100° C. or more, is provided so that, accordingly, the stretch blow molding can be conducted at higher temperature of the mold temperature described in the conventional method.

SUMMARY OF THE INVENTION

Accordingly, the inventors have discovered the new method that if the temperature of the injection molded preform is 100° C. or more at the outer surface temperature, the inner side temperature of cooled preform by the injection core with rise of temperature by the internal part heat can get near with the outer side temperature drop by a heat dissipation and also the preform temperature can be kept to longer period in the temperature region of a stretch blow molding temperature.

Accordingly an object of the present invention is to provide a new method that the temperature distribution of the inner side of the body wall of the injection molded preform is changed to the gentle gradient slope shape temperature distribution from the mountain shape not by the external application of heating but by the preform itself so that as the hot parison method the bottle which the top load value is improved by the stretch blow molding is capable to be provided.

The present invention is a method for injection stretch blow molding, which comprises the steps of:

-   -   injecting and filling a molten material resin into a cavity         being formed by an injection cavity mold, a neck mold, and an         injection core;     -   forming a closed-end preform of a body part and a neck part         integrally, by quick cooling the melt in the cavity by both the         injection cavity mold and the injection core;     -   mold-releasing the preform from the injection cavity mold         together with the injection core while the body part and a         bottom part are in a high temperature state;     -   continuing cooling the inner side of the preform by said         injection core simultaneously being to be transferring the         preform with the injection core;     -   terminating the cooling of the inner side of the preform by         mold-release of the injection core after a transfer halting;     -   holding the preform at the neck part after mold-release of the         injection core, and maintaining a holding time, as a         temperature-averaging time of the preform, until the outer         surface temperature of said preform drops to the predetermined         stretch blow molding temperature after passing the peak         temperature; and     -   stretch blow molding the preform to a thin-wall hollow molded         article in the mold temperature region.

Further, the present invention is a method for injection stretch blow molding, which comprises the steps of:

-   -   injecting and filling a molten polyethylene terephthalate into         the cavity being formed by the injection cavity mold, neck mold,         and injection core;     -   forming a closed-end preform of the body part and the neck part         integrally with3 mm to 5 mm thickness of the body part, by quick         cooling the melt for 2 seconds to 10 seconds in the cavity being         set of the temperature 3° C. to 20° C. by both the injection         cavity mold and the injection core;     -   mold-releasing the preform from the injection cavity mold         together with the injection core while the body part and the         bottom part are in the high temperature state;     -   continuing cooling the inner side of the preform by said         injection core for 4 seconds to 14 seconds depending on the body         part thickness simultaneously being to be transferring the         preform with the injection core;     -   terminating the cooling of the inner side of the preform by         mold-release of perform from the injection core;     -   holding the preform at the neck part after mold-release of the         injection core, and maintaining a holding time, as a         temperature-averaging time of the preform, until the outer         surface temperature of said preform drops to the predetermined         stretch blow molding temperature of between 133° C. to 100° C.         after passing the peak temperature; and     -   stretch blow molding the preform in the mold temperature region         to the thin-wall hollow molded article of the body part         thickness t′ having average thickness of 0.28 mm to 0.33 mm.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1A is a diagram showing an injection process of the molding method according to the present invention.

FIG. 1B is a diagram showing an inner cooling process of the molding method according to the present invention.

FIG. 2A is a diagram showing a temperature-averaging process of the molding method according to the present invention.

FIG. 2B is a diagram showing a stretch blow molding process of the molding method according to the present invention.

FIG. 3 is a front view of a bottle measured for a top load value.

FIG. 4 is a graph described an outer surface temperature after a cavity mold-release of a preform having a body part thickness t=3 mm together with Comparative Example.

FIG. 5 is a graph described an outer surface temperature after a cavity mold-release of a preform having a body part thickness t=4 mm together with Comparative Example.

FIG. 6 is a graph described an outer surface temperature after a cavity mold-release of a preform having a body part thickness t=5 mm together with Comparative Example.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

FIGS. 1A, 1B, 2A and 2B illustrate one example of a mold apparatus used for the stretch blow molding method according to the present invention.

An injection cavity mold 1 molds the outer side of a closed-end perform 10 and has a cooling channel in the internal part and an injection nozzle at a bottom part. In an opened upper edge side of the injection cavity mold 1 neck molds 3 which forms a neck part of the perform 10 is provided at the under side of a base plate 4 to openable and closable in the right and left.

An injection core 15 molds the inner side of the perform 10 and is made to set in downward direction to the under side of a clamping block 6 provided in movable up and down at the upper part of the injection cavity mold 1 and a cooling channel is provided in the internal part of the injection core. The clamping block 6 is provided to a transfer plate which moves 180° reciprocating movable up and down, not shown in-the drawings, and by the transfer plate, the injection core 5 moves downward together with the mold clamping block 6 to be inserted into the injection cavity mold through the neck molds 3 from a hole part 4 a which is provided in drilling to the base plate 4, and a cavity 7 which the closed-end preform 10 is injection-molded in the cavity sides therebetween, is formed.

A blow mold 8 for molding a bottle is provided by a pair of split-cavity molds with openable and closable in the right and left, and a bottom mold 11 is provided at the center of the bottom part of the blow cavity 9. The upper side aperture periphery is made to be a concave point in which holders 12 of supporting the neck part of the preform 10 are fitted.

Ejecting plates 13 combine with a support of the preform 10 by a pair of plate bodies opening and shutting to the right and left, not shown in the drawings, which is provided in reciprocating transferable from a halting position of the preform 10 to the central upper part of the blow mold 8 and also in a vertically movable to the blow mold 8, and to the under side of the hole parts 14 which are provided in drilling to the butting edge of the plate body, the above mentioned holders 12 are provided separately to a pair of plate bodies.

A blow core 15 is provided to a vertical movement block 16 which is provided to the hole part upper part of the ejecting plates 13 in downward direction, and in the internal part center, a stretch rod 17 is inserted in movable up and down, and an air flow gap is provided in the periphery of the stretch rod 17. It is made to comprise that the stretch rod 17 moves vertically together with the blow core 15, and that thereafter being fitted into the internal side neck part of the preform 10, the blow core 15, independently, extends to the mold side of the above mentioned bottom mold 11.

Then, a molding process of polyethylene terephthalate (PET) as a molding resin is explained as one example.

Initially, as shown in FIG. 1A, molten (254° C.) polyethylene terephthalate is injected and filled from the injection nozzle 2 into the cavity 7 formed by mold clamping, and the melt 10 a generated in the cavity 7 is rapidly cooled by both the injection cavity mold 1 and the injection core 5 which are set in the temperature 3° C. to 20° C. The cooling temperature 3° C. is the lower limit temperature in case of accelerating the cooling rate, and 20° C. is the upper limit temperature which is set when the temperature or humidity of the molding environment is high. The set temperature in general is 15° C.±3° C.

As for the neck molds 3, since the thickness of neck part of the preform 10 is thinner than the body part, by the heat transfer which is generated while the neck molds 3 are in contact with the injection cavity mold 1 by the mold clamp, the neck part is solidified by cooling until the mold-release so that a cooling means is not provided.

The melt 10 a is formed to the preform 10 by rapid cooling (hereinafter called an injection cooling) from both the cooling by the injection cavity mold 1 (hereinafter called an outer side cooling) and the cooling by the injection core 5 (hereinafter called an inner side cooling). The injection cooling time is different depending upon the thickness of the body part, but is limited within the time while the cooling in the inside of the body wall is incomplete in a high temperature state, and the mold-release is possible from the injection cavity mold 1 together with the injection core 5 in sticking.

The injection cooling time is preferable, in case of the average body part thickness t=3 mm (hereinafter called t=3), 2 seconds to 5 seconds, in case of t=4 mm (hereinafter called t=4), 5 seconds to 8 seconds, in case of t=5 mm (hereinafter called t=5), 6 seconds to 10 seconds, from the point of ensuring the internal part heat. If the injection cooling is conducted longer than the above mentioned time, the region of the outer side skin layer caused by cooling increases and the high temperature region of the internal part becomes narrow and heating softening of the inner and outer surface layers by the internal part heat after cavity mold-release is difficult to conduct so that before the stretch blow molding, the heating temperature control to the entire preform by an outer part heat is required.

After the above mentioned injection cooling time, as shown in FIG. 1B, the mold-release of the neck part is conducted by opening the neck molds 3 to the right and left, and then the mold clamp block 6 is moved upward and the injection core 5 is mold-released (hereinafter called a cavity mold release) to draw from the injection cavity mold 1 together with the preform 10. The outer surface temperature of the preform 10 after the mold-release (after approximately 2 seconds), is preferably 105° C. to 120° C. in the case of t=3, 91° C. to 96° C. in the case of t=4, and 88° C. to 97° C. in the case of t=5.

During the cavity mold-release, even if the skin layer thickness generated in the outer side of the preform 10 is thin, in the periphery of the injection core 5, by the shrinkage of the inner side of the preform by rapid cooling, the preform 10 sticks so as to embrace to the injection core 5 tightly and the preform 10 is mold-released together with the injection core 5 from the injection cavity mold 1 so that the form of the preform 10 is not made so as to be impaired by the cavity mold-release. After the mold-release the preform 10 is transferred together with the injection core 5 at the halting position which is located in opposite to the injection cavity mold 1 by 180 degrees rotating-turn of the transfer plate, not shown in the drawings.

By this cavity mold-release, a cooling of the preform 10 from the outer side terminates and the skin layer of the outer surface exposed to an atmosphere disappears by heat dissipation and the outer surface temperature rises to the peak temperature. On the other hand, to the injection core 5 stuck by the preform 10, until being mold-released from the injection core (hereinafter called a core mold-release) for the setting time, the preform 10 is cooled by the inner side continuously from the injection. Accordingly, the temperature distribution in the inside of the body part wall of the preform 10 varies from the mountain shape which the center is high by cooling from both sides at the cavity mold-release, to the slope shape of the temperature gradient which is high in the outer side and is low in the inner side.

The cooling time of the inner side is preferable to select according to the above mentioned injection cooling time in the region, for example, preferably 4 seconds to 8 seconds for the body thickness t=3, 6 seconds to 8 seconds for t=4, 8 seconds to 12 seconds for t=5, and if the inner side cooling is conducted longer than the above mentioned time which is set to objecting the injection cooling time, the cooling proceeds in deep from the inner side to the internal part so that as a whole the super cooling is made.

Giving one example, in the case of t=4 and injection cooling time 5 seconds, the cross section temperature of the body wall of the preform at after approximately 3 seconds from mold-release is 130.51° C. at the outer side temperature, 143.71° C. at the central temperature and 132.25° C. at the inner side temperature, so that the temperature distribution in the inside of the body wall shows the mountain shape which the center is high. Then, when the inner side cooling is given by the injection core 5 for 10 seconds, the cross section temperature after mold-release falls insomuch as 116.02° C. at the outer side temperature, 111.96° C. at the central temperature, 89.20° C. at the inner side temperature, so that the temperature distribution in the inner side of the body wall is steep gradient slope shape which the inner side is extremely low and the temperature difference of the inner and outer sides shows as much as 26.82° C. The temperature difference of the inner and outer sides is small over time with the inner side temperature rise of the internal part heat and the heat dissipation from the outer surface, and the inner side skin layer which is generated in thick is softening, but the entire preform temperature drops so low that a reheating before the stretch blow molding is required.

Even if the inner side cooling time is in the above mentioned setting region, since the inner side of the preform 10 is in a supercooling state, when the stretch blow molding is conducted immediately after the core mold-release, an uneven thickness occurs and a bottle having uniform thickness distribution can not be molded. Then, after a lapse of the inner side cooling time, the ejecting plates 13 are moved to the halting position of the preform 10, and the preform 10 is held between the holders 12 at the neck part. Subsequently to the holding, the ejecting plate moves upward, and the injection core 5 is drawn from the preform 10 and by the mold-release the cooling is terminated. After the core mold-release is over, the preform 10 of a hollow state is transferred to the upper central part of the blow mold 8 by the ejecting plates 13, and at that position the temperature-averaging of the preform 10 is conducted as the process prior to the stretch blow molding.

By the temperature-averaging process the preform 10 is left in the hollow state until the outer surface temperature of the preform 10 drops, from the peak temperature (121° C. to 135° C. in the case of t=3, 111° C. to 125° C. in the case of t=4, 125° C. to 135° C. in case of t=5), to the temperature region (123° C. to 118° C. in the case of t=3, 124° C. to 107° C. in the case of t=4, 134° C. to 129° C. in the case of t=5)which is capable to conduct the stretch blow molding in suitable for the improvement of the top load.

Since the temperature-averaging time is, by the inner part heat kept in the preform 10, the time that the inner side thick skin layer caused by contact with the injection core 5 is heated and softened and simultaneously the inner side temperature is raised, in the body wall within the time, the inner side is applied heating by the internal part heat, and the thick formed skin layer is conducted to get softening. Also, in the hollow preform which the neck part is merely opened, the dissipated heat from the inner side surface tends to keep in, and by the heat accumulation in the inside of the preform, heating application of the skin layer is conducted efficiently and the like, so that in course of time until the outer surface temperature attains to the stretch blow molding temperature after passing the peak, by the inner side temperature rise and the outer side temperature drop, the gradient temperature difference in the body wall becomes small to be gentle gradient, and the temperature gradient becomes homogeneity state as a whole. It is needless to say that the difference in the time attained to the stretch blow molding temperature depends on the setting condition of temperature and time.

The time that the outer surface temperature is maintained in the stretch blow molding temperature region is longer in comparison with the time that drops from the peak temperature to the stretch blow molding temperature region, and in such molding temperature region, the stretch blow molding is capable to be conducted without the time limit from the cavity mold-release. However, if considering the productivity as the mold cycle, a short time is preferable to conduct.

Since the mold temperature region is determined by passage of time from the cavity mold-release, the temperature-averaging time amounts to be the remaining time which the time from the cavity mold-release until the stretch blow molding is subtracted by the inner cooling time for each preform.

When the temperature-averaging time is over, as shown in FIG. 2B, the ejecting plates 13 move downward to the mold upper side position, and also, before or after the blow mold 8 shuts, the upward blow core 15 moves downward together with the vertical movement block 16, and the stretch rod 17 is inserted to the preform 10 and the neck molds 3 and the blow mold 8 and the blow core 15 are conducted to mold clamping.

After in doing so, by an elongation of the vertical stretch of the stretch rod 17 and air blow from the blow core 15, the preform 10 is expanded to the cavity surface of the blow cavity 9, and is molded to a bottle having thin body part thickness t′ (0.25 mm to 3.5 mm) A detail body part shape of the bottle 20 is omitted in FIGS. 2A and 2B, but as the bottle for beverage, as shown in FIG. 3, in six spots of the side of the body part 21, the bottle which elliptical panels 22 are provided to concave in vertical long is used.

When the bottle 20 having such form is molded through the above mentioned processes and subsequently measured on the top load value, the results are high values such as 172 to 185 N at the body part thickness of the preform 10 (t)=3, 281 to 310 N to t=4 and 283 to 325 to t=5. The improvement of the top load values is speculated as a result that by continuation of the inner side cooling by the injection core 5, the temperature distribution varies from the mountain shape to slope shape of the temperature gradient having low inner side temperature, and the temperature gradient becomes gradual by the temperature-averaging time after the core mold-release, and also the temperature difference in the body wall is small, so that the difference of degree of orientation depending on temperature becomes small, and the formation of multiple layers (inner side, central part, outer side) of the body wall which is easily generated in the mountain shape temperature distribution, is not occurred.

As for the 500 ml bottle for beverage with the above mentioned panels, the top load value based on the bottle weight (preform weight) is considered to be preferable to have 170N or more at the preform body part thickness t=3, 280N or more at t=4 and t=5, so that the top load value which is in excess of the preferable value is capable to be evaluated. Accordingly, even by the stretch blow molding of the hot parison method, by the inner side cooling by the injection core and the subsequent temperature-averaging time setting, the thin wall thickness PET bottle which is improved to the top load value can be obtained.

Examples are explained as following.

Example: Preform: Material for molding: polyethylene terephthalate (PET), Manufactured by Eastman Chemical Company (9921W) Dimensions: Opening diameter: φ21 mm Thickness (t): three samples: 3 mm, 4 mm, 5 mm Body diameter (central part): φ23.1 mm Stretch part length: 74 mm(for t = 3 mm, t = 4 mm) 62 mm(for t = 5 mm) Weight t = 3 mm 23.8 g t = 4 mm 30.6 g t = 5 mm 30.6 g Molding condition 1: (Preform injection molding) Barrel heater set temperature 270° C. Injection time t = 3 mm  6 seconds t = 4 mm 10 seconds t = 5 mm 13 seconds Injection mold temperature, Injection core temperature (chiller) 15° C.

Cooling and Averaging time (seconds) Injection cooling Inner side Averaging T(mm) (both sides) cooling (leaving) 3 2 to 5 2 to 8 4 or more 4 5 to 8 5 to 8 7 or more 5 7 to 10 5 to 8 8 or more

Molding condition 2: (Stretch blow molding) Molding temperature (Outer surface temperature) Atmospheric temperature is 22° C.. t = 3 mm 120° C. to 100° C. t = 4 mm 120° C. to 100° C. t = 5 mm 133° C. to 115° C. Blow air pressure 2.2 MPa Stretch Ratio (vertical) 2.5 (t = 3 mm, t = 4 mm) 3.0 (t = 5 mm) Stretch Ratio (horizontal) 2.98 Molded article: Bottle for beverage 500 ml (body part six sides with panels, Refer to FIG. 4) Dimensions: Opening diameter φ21 mm Body diameter (Maximum) φ68.9 mm Average thickness t′ = 0.28 mm (for t = 3 mm) t′ = 0.32 mm (for t = 4 mm) t′ = 0.33 mm (for t = 5 mm) Molding machine used: AOKI-100LL-20 Temperature measuring instrument: Infrared thermograph TVS-2000MK2 (Manufactured by Nippon Avionic Co., Ltd. Top load measuring instrument: Tensile compression testing instrument TCM-200 (Manufactured by Minebea Co., Ltd.)

FIG. 4 is shown, as for the outer surface temperature after the cavity mold-release of the injection molded preform(t=3 mm) under the molding condition 1 and the top load value of the obtained bottle which the preform is molded by the stretch blow molding at the molding temperature region (120° C. to 100° C.) under the molding condition 2, in five Examples wherein A1, A2, A3, A4, and A5 are made to differ the cooling time(second) and temperature-averaging time(second) in the injection time 6 seconds, together with Comparative Example A0. Here, the temperature-averaging time of A0 is the time from the cavity mold-release to the molding (considering time). Cooling Inner Side Temperature- time Cooling time averaging Top Load Value (second) (second) time (second) (Newton) A1 2 7 12, 16, 34 172, 177, 177 A2 2 8 8, 10, 28 173, 178, 177 A3 3 5 8, 10, 40 174, 175, 178 A4 3 6 6, 8, 30 176, 178, 176 A5 3 4 7, 15, 39 172, 176, 177 A0 4 0 8, 20, 32 161, 164, 169

FIG. 5 is shown, as for the outer surface temperature after the cavity mold-release of the injection molded preform(t=4 mm) under the molding condition 1 and the top load value of the obtained bottle which the preform is molded by the stretch blow molding at the molding temperature region (120° C. to 100° C.) under the molding condition 2, in five Examples wherein B1, B2, B3, B4, and B5 are made to differ the cooling time and temperature- averaging time (second) in the injection time 10 seconds, together with Comparative Example B0 as the conventional method which the inner side cooling by the injection core is not conducted. Here, the temperature-averaging time of B0 is the time from the cavity mold-release to the molding. Cooling Inner Side Temperature- time Cooling averaging Top Load Value (second) time(second) time(second) (Newton) B1 5 6 12, 22, 36 280, 290, 314 B2 5 8 8, 10, 28 284, 292, 299 B3 6 6 8, 12, 24 281, 290, 304 B4 7 6 10, 16, 24 281, 291, 299 B5 7 8 10, 16, — 281, 293, — B0 8 0 8, 24, 30 277, 278, 275

FIG. 6 is shown as for the outer surface temperature after the cavity mold-release of the injection molded preform (t=5 mm) under the molding condition 1 and the top load value of the obtained bottle which the preform is molded by stretch blow molding at the molding temperature region (125° C. to 115° C.) under the molding condition 2, in three Examples wherein C1, C2, and C3 are made to differ the cooling time and the temperature-averaging time (second) in the injection time 13 seconds, together with Comparative Example C0 as the conventional method which the inner side cooling by the injection core is not conducted. Here, the temperature-averaging time of C0 is the time from the cavity mold-release to the molding. Cooling Inner Side Temperature- time Cooling time averaging Top Load Value (second) (second) time (second) (Newton) C1 6 8 16, 20, 32 283, 298, 305 C2 6 12 10, 14, 20 288, 320, 325 C3 8 8 8, 16, 20 285, 295, 302 C0 8 0 8, 24, 28 270, 275, 276

As in FIG. 4 to FIG. 6, it is obvious that, generally, the longer averaging time is, the top load value is made to be higher. This is caused by the temperature difference of the inner and outer sides being made to be small to approach equivalent over time, and also no difference is made in the stretch degree so that the body wall is constituted in a single layer.

However, in case of Comparative Examples A0, B0, C0 which the inner side cooling is not conducted, even if the stretch blow molding is conducted in the molding temperature region after the peak temperature, the top load values are not improved. In the temperature distribution after the cavity mold-release in Comparative Examples, the central part is the high temperature mountain shape, and even if the outer surface temperature drops to the molding temperature region, the temperature distribution is the same as the mountain shape, and the orientation degree of molecular orientation by stretch is low as temperature rise, so that from the difference of the orientation degree, the body wall is made to be formed into three layers(inner side, center side, outer side) although not so notable, and this is speculated to affect the compression strength. TABLE 1 Stretch Blow Stretch Blow Stretch Blow Peak Temperature Molding(1) Molding(2) Molding(3) Time to Time Time Time Peak From From From Thick- Temper- Temper- Mold- Temper- Top Mold- Temper- Top Mold- Temper- Top ness Mark Condition ature ature Release ature Load Release ature Load Release ature Load A1  6 + 2 + 7 134.08 6 19 119.04 172 23 114.52 177 41 106.15 177 t = 3 A2  6 + 2 + 8 133.60 7 16 122.31 173 18 119.45 178 36 102.63 177 A3  6 + 3 + 5 126.40 7 13 120.92 174 15 117.23 175 45 101.06 178 A4  6 + 3 + 6 126.29 7 12 120.61 176 14 117.39 178 36 100.97 176 A5  6 + 4 + 4 120.96 6 11 118.89 172 19 112.21 176 43 102.88 177 B1 10 + 5 + 6 124.07 11 18 122.61 282 28 117.12 290 42 112.27 314 t = 4 B2 10 + 5 + 8 124.54 12 16 123.28 284 18 121.98 292 38 110.63 299 B3 10 + 6 + 6 118.43 11 14 117.91 281 18 116.07 290 30 108.85 304 B4 10 + 7 + 6 112.72 12 16 109.67 281 22 106.10 291 30 102.05 299 B5 10 + 7 + 8 111.80 11 18 107.36 281 24 103.50 293 C1 13 + 6 + 8 134.49 18 24 133.93 283 28 132.24 298 40 128.52 305 t = 5 C2 13 + 6 + 12 133.10 18 22 132.72 288 26 131.72 320 32 130.01 325 C3 13 + 8 + 8 128.90 16 20 128.50 285 24 128.20 295 28 127.09 302 Remarks: Condition(time) Injection + cooling + inner side cooling Time(second) Temperature (° C.) Top Load (N)

In Table 1, the molding condition of the above mentioned each Example and the peak temperature and time, molding time from the cavity mold-release, molding temperature, top load value and the like are listed as in table where the time from the mold-release is described as the preform being drawn from the cavity mold together with the injection core until the stretch blow molding being started (inner side cooling time+temperature-averaging time). It is obvious from the table that, even if the body thickness of the preform varies, if the outer surface temperature is on way of dropping after the maximum peak, the top load value is said to be higher than 170N at t=3 mm, 280N at t=4 mm, t=5 mm which is regarded as the above mentioned standard value. TABLE 2 Peak Temperature Stretch Blow Molding Time to Peak Time From Top Thickness Mark Condition Temperature Temperature Mold Release Temperature Load t = 3 A0  6 + 5 + 0 114.43 11 8 114.10 161 t = 4 B0 10 + 8 + 0 111.05 11 8 108.14 276 t = 5 C0 13 + 10 + 10 125.58 18 8 119.22 270

It is obvious that the comparison of conventional method shown in Comparative Examples in Table 2. In the conventional method which is conducted by the stretch blow molding in the molding temperature before the surface temperature reaches to the peak temperature, the top load values are 161N at t=3 mm, 278N at t=4 mm and 270N at t=5 mm. Accordingly, the present invention is extremely useful as the hot parison method stretch blow molding, from the point of the top load improvement in the bottle having thin body part.

As for the above mentioned Examples, while polyethylene terephthalte is used as a base resin, the present invention is applicable to the thermoplastics resins such as polyethylene naphthalate, polycarbonate, polypropylene, polyethylene and the like which enable to stretch blow mold by the hot parison method, therefore, the present invention is not limited to polyethylene terephthalte as the base resin, and also, since the present invention is applicable to a wide-mouth bottle as a hollow molded article, the present invention is not limited only to a bottle. 

1. A method for injection stretch blow molding, which comprises the steps of: injecting and filling a molten material resin into a cavity being formed by an injection cavity mold, a neck mold, and an injection core; forming a closed-end preform of a body part and a neck part integrally, by quick cooling the melt in the cavity by both the injection cavity mold and the injection core; mold-releasing the preform from the injection cavity mold together with the injection core while the body part and a bottom part are in a high temperature state; continuing cooling the inner side of the preform by said injection core simultaneously being to be transferring the preform with the injection core; terminating the cooling of the inner side of the preform by mold-release of the injection core after a transfer halting; holding the preform at the neck part after mold-release of the injection core, and maintaining a holding time, as a temperature-averaging time of the preform, until the outer surface temperature of said preform drops to the predetermined stretch blow molding temperature after passing the peak temperature; and stretch blow molding the preform to a thin-wall hollow molded article in the mold temperature region.
 2. A method for injection stretch blow molding, which comprises the steps of: injecting and filling a molten polyethylene terephthalate into the cavity being formed by the injection cavity mold, neck mold, and injection core; forming a closed-end preform of the body part and the neck part integrally with 3 mm to 5 mm thickness of the body part, by quick cooling the melt for 2 seconds to 10 seconds in the cavity being set of the temperature 3° C. to 20° C. by both the injection cavity mold and the injection core; mold-releasing the preform from the injection cavity mold together with the injection core while the body part and the bottom part are in the high temperature state; continuing cooling the inner side of the preform by said injection core for 4 seconds to 14 seconds depending on the body part thickness simultaneously being to be transferring the preform with the injection core; terminating the cooling of the inner side of the preform by mold-release of perform from the injection core; holding the preform at the neck part after mold-release of the injection core, and maintaining a holding time, as a temperature-averaging time of the preform, until the outer surface temperature of said preform drops to the predetermined stretch blow molding temperature of between 133° C. to 100° C. after passing the peak temperature; and stretch blow molding the preform in the mold temperature region to the thin-wall hollow molded article of the body part thickness t′ having average thickness of 0.28 mm to 0.33 mm. 